Salts of polyaspartic acid by high temperature reaction

ABSTRACT

Polyaspartate, useful for inhibition of incrustations due to materials causing hardness in water and of value in detergent formulations, can be prepared by reacting maleic acid or fumaric acid in a molar ratio of 1:1-2.1 at temperatures greater than 190° C., followed by conversion of the polymer formed in this reaction to a salt of polyaspartic acid by basic hydrolysis.

CROSS-REFERENCE TO RELATED APPLICATIONS AND PATENTS

The present application is a divisional of U.S. patent application Ser. No. 08/692,768, filed on Aug. 6, 1996 (now U.S. Pat. No. 5,773,565), which is a continuation of application Ser. No. 08/287,154 filed on Aug. 8, 1994 pending, which is a continuation of application Ser. No. 08/199,652 filed on Feb. 22, 1994 (now U.S. Pat. No. 5,367,047), which is a divisional of application Ser. No. 08/007,376 filed on Jan. 21, 1993 (now U.S. Pat. No. 5,288,783), which is a CIP of application Ser. No. 07/882,919 filed on May 14, 1992 (now abandoned).

FIELD OF THE INVENTION

This invention relates to a process for the production of polyaspartic acid and its salts and the use of these materials.

DESCRIPTION OF RELATED ART

The salts of polyaspartic acid have been used for fertilizers, and scale inhibition agents. They are particularly useful for the prevention of scale deposition in boiler water, reverse osmosis membranes and in detergents. One of the primary characteristics that makes them valuable in this respect is the fact that they are readily biodegradable, whereas other materials that are presently used for this purpose are either slowly biodegradable, e.g. polyacrylic acid, or harmful to the environment, e.g. polyphosphoric acid.

Sodium polyaspartate was used in the prevention of boiler scale by changing the crystal structure of calcium salts resulting in the formation of a soft scale (Sarig et al, The use of polymers for retardation of scale formation. Natl Counc Res Dev [Rep] (Isr.), 150, 1977). Polyaspartic acid, molecular weight (MW) 6,000, was found to be superior to polyglutamate, MW 14,400, polyvinyl sulfonate, MW 5300, and polyacrylic acid, MW 6,000, in that it gave 66% retardation of total scale and 90% retardation of calcium sulfate scale. In addition, the scale formed in the presence of polyaspartate was softer than that produced in the presence of polyacrylate, polyglutamate and polyvinyl sulfonate.

U.S. Pat. No. 4,839,461 discloses a method for making polyaspartic acid from maleic acid and ammonia by reacting these constituents in a 1:1-1.5 molar ratio by raising the temperature to 120°-150° C. over a period of 4-6 hours and maintaining it for 0-2 hours. It is further disclosed that temperatures above 140°-160° C. result in elimination of CO₂, thus teaching degradation of the material. The molecular weight range obtained by this method was said to be 1,000-4,000 with a duster at 1,800-2,000. That patent states that this material is useful in the prevention of tarnishing glass and porcelain articles. Although not stated in this patent, it is known that this action would occur as a result of the inhibition of calcium sulfate deposition. Harada, et al (Thermal polycondensation of free amino acids with polyphosphoric acid. Origins Prebiol. systems Their Mol Matrices, Proc. Conf., Wakulla Springs, Fla., 289, 1963) obtained polyaspartic acid from aspartic acid and phosphoric acid at temperatures over 100° C. over a time period of 50-250 hrs, but required temperatures over 170° without phosphoric acid being present.

U.S. Pat. No. 5,057,597 discloses a method for the polycondensation of aspartic acid to produce polyaspartic acid by heating the aspartic acid in a fluidized bed reactor to 221° C. for a period of 3-6 hours in a nitrogen atmosphere followed by conventional alkaline hydrolysis.

Kovacs et al. (J. Org. Chem., 25 1084 [1961]) prepared polyaspartic acid by heating aspartic acid to 200° C. in vacuo for a period of 120 hours or in boiling tetralin over a period of 100 hours. Kovacs et al, showed that the intermediate formed in the thermal polymerization of aspartic acid was polysuccinimide.

Frankel et al. (J. Org Chem., 16, 1513 [1951]) prepared polyaspartic acid by heating the benzyl ester of N-carboxyanhydroaspartic acid followed by saponification.

Dessaigne (Comp. rend. 31, 432-434 [1850]) prepared condensation products which gave aspartic acid on treatment with nitric or hydrochloric acid by dry distillation of the acid ammonium salts of malic fumaric or maleic acid at unspecified times and temperatures.

SUMMARY OF THE INVENTION

Polymers of aspartic acid which are suitable for the prevention of scale may be obtained by reacting maleic acid and ammonia in a molar ratio of 1:1-2.1 at 200°-300° C. and then converting the polysuccinimide formed to a salt of polyaspartic acid by hydrolysis with a metal hydroxide. The reaction is carried out by the addition of water to maleic anhydride, thus forming maleic acid, or to maleic acid followed by addition of the appropriate amount of ammonia in the form of gaseous ammonia or as its aqueous solution. This solution is then heated to remove water. A melt of the maleic acid and ammonia is formed and water removal continues as the reaction proceeds and the temperature is brought to 200°-300° C. When the theoretical quantity of water formed in the production of polysuccinimide has been removed, which may occur in less than 5 minutes, the reaction mixture is allowed to cool. The polysuccinimide formed can be used to make other useful products or can be hydrolyzed with metal hydroxides to provide the appropriate salt of polyaspartic acid. Solutions of the salts of polyaspartic acid formed in this manner have the same scale inhibition performance and molecular weight range as do the polymers formed by the thermal polymerization of aspartic acid itself. Further manipulation to remove the water or the salts can be carried out to provide water free powders of the salts or the free acid.

The polyaspartic acid provided by the present invention is suitable for inhibition of scale deposition, whereas the methods previously used to produce polyaspartic acid did not provide a polymer of sufficient molecular weight to prevent scale formation.

The object of this invention is to provide a means of preparing polysuccinimide. A further object of this invention is to provide a means of preparing salts of polyaspartic acid.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 shows the effect of additives on the inhibition of calcium carbonate precipitation.

FIG. 2 shows the effect of thermally polymerized mono-ammonium maleate salts as calcium scale inhibitors.

FIG. 3 shows the effect of thermally polymerized mono-ammonium fumarate salts as calcium scale inhibitors.

FIG. 4 shows the effect of thermally polymerized di-ammonium fumarate and maleate salts as calcium scale inhibitors.

FIG. 5 shows the calibration of a molecular weight column.

FIG. 6 shows the molecular weight determination of polymers formed in Examples 2, 4, 10, and 11.

FIG. 7 shows the molecular weight determination of polymers formed in Examples 6, 8, 12, and 13.

FIG. 8 shows the molecular weight determination of polymers formed in Examples 3 and 7

DETAILED DESCRIPTION OF THE EMBODIMENTS

As opposed to the teachings of U.S. Pat. No. 4,839,461, I have found that, although the use of the polyaspartic made by the process is said to be useful in the prevention of hardness deposits, no actual experimentation to confirm this finding is reported. In fact, upon careful repetition of the procedures of U.S. Pat. No. 4,839,461, the results below clearly demonstrate that polymers of aspartic acid prepared by heating the ammonium salts of maleic acid at 140°-150° C. for 4 to 6 hours did not give a polymer that was active as a calcium scale inhibitor. Further, when calculations of the theoretical weight of polysuccinimide (molecular weight 97) formed in Example 1 indicates that the reaction was not taken to completion under the conditions described.

EXAMPLE 1 Thermal Polymerization of L-Aspartic Acid at 240°-250° C.

Aspartic acid, 133 g, was tumbled under nitrogen at 100 Torr, at 240°-250° C. for 1.5 hours to give a pink powder weighing 97.3 g. This solid was slurried in 200 ml of water at 25° C. and a solution of 40 g of water containing 40.0 g of sodium hydroxide was added over a period of 15 minutes with intermittent cooling to keep the temperature between 60° and 70° C. The resultant clear red-brown solution, pH 12.0, was adjusted to pH 7.0 by the addition of 1.5 g of citric acid and contained 25% solids.

The sodium polyaspartate was tested for inhibition of calcium carbonate precipitation by the calcium drift assay. In this assay a supersaturated solution of calcium carbonate is formed by adding 29.1 ml of 0.55 M NaCl and 0.01 M KCl to 0.15 ml of 1.0 M CaCl₂ and 0.3 ml of 0.5 M NaHCO₃. The reaction is initiated by adjusting the pH to 7.5-8.0 by titration with 1 N NaOH and addition of the material to be tested for inhibition of CaCO₃ precipitation at a level of 1.7 ppm. At three minutes, 10 mg of CaCO₃ is added and the pH is recorded. The decrease in pH is directly correlated to the amount of CaCO₃ that precipitates. The effectiveness of the inhibition is compared to that of sodium polyacrylate, used commercially for the purpose of preventing scale formation.

FIG. 1 shows the effect of no additive in this test compared with polyacrylate, chemically synthesized L-α-polyaspartate and the polyaspatate prepared in this Example. Both thermally prepared and chemically synthesized polyaspartate were very close to polyacrylate by the calcium drift assay when all materials were tested at 1.7 ppm of additive.

EXAMPLE 2 Thermal Polymerization of Mono-Ammonium Maleate at 145°-150° C.

Following the examples of U.S. Pat. No. 4,839,461, a slurry of 9.8 g (0.1 mole) maleic anhydride was dissolved in 20 ml water at 80°-95° C. and stirred for 30 minutes while allowing the mixture to cool to 25° C. To this colorless solution at 25° C. was added 13 g of 30% aqueous solution of ammonium hydroxide (0.11 mol NH₃) to give a colorless solution. This solution was boiled to dryness over a period of 30 minutes at approximately 100°-115° C. to give a white crystalline solid. The solid was tumbled under nitrogen at 100 Torr, at 145°-150° C. for 4 hours to give a water insoluble, pinkish-tan brittle grasslike solid weighing 11.4 g. This solid was dissolved in 26.2 g of an aqueous solution containing 1.36 g of sodium hydroxide to form a clear red-brown solution, pH 7.0, containing 25% solids.

FIG. 2 shows a plot of the data obtained in this example compared to that of the no additive assay and the thermally prepared polyaspartate. The material obtained at 145°-150° C. is no better than no additve when tested at 1.7 ppm.

EXAMPLE 3 Thermal Polymerization of Mono-Ammonium Maleate at 190°-200° C.

A slurry of 9.8 g (0.1 mole) maleic anhydride was dissolved in 20 ml water at 80°-95° C. and stirred for 30 minutes while allowing the mixture to cool to 25° C. To this colorless solution at 25° C. was added 13 g of 30% aqueous solution of ammonium hydroxide (0.11 mol NH₃) to give a colorless solution. This solution was boiled to dryness over a period of 30 minutes at approximately 100°-115° C. to give a white crystalline solid. The solid was tumbled under nitrogen at 100 Torr, at 190°-200° C. for 4 hours to give a water insoluble, pinkish-tan brittle glasslike solid weighing 10.6 g. This solid was dissolved in 35.4 g of an aqueous solution containing 1.9 g of sodium hydroxide to form a dear red-brown solution, pH 9.0, containing 25% solids.

FIG. 2 shows that polyaspartic acid of this example in the calcium drift assay of Example 1 at 1.7 ppm much improved compared to the material of Example 2.

EXAMPLE 4 Thermal Polymerization of Mono-Ammonium Maleate at 240°-250° C.

A slurry of 9.8 g (0.1 mole) maleic anhydride was dissolved in 20 ml water at 80°-95° C. and stirred for 30 minutes while allowing the mixture to cool to 25° C. To this colorless solution at 25° C. was added 13 g of 30% aqueous solution of ammonium hydroxide (0.11 mol NH₃) to give a colorless solution. This solution was boiled to dryness over a period of 30 minutes at approximately 100°-115° C. to give a white crystalline solid. The solid was tumbled under nitrogen at 100 Torr, at 240°-250° C. for 1.5 hours to give a water insoluble, pinkish-tan brittle grasslike solid weighing 9.6 g. This solid was dissolved in 36.0 g of an aqueous solution containing 4.0 g of sodium hydroxide to form a clear red-brown solution, pH 12.0. To this solution was added 0.25 g citric acid to adjust the pH to 8.5 and the resultant solution contained 25% solids.

FIG. 2 shows that the polyaspartic acid of this example in the calcium drift assay of Example 1 at 1.7 ppm was equivalent to that of thermally prepared polyaspartate.

EXAMPLE 5 Thermal Polymerization of Mono-Ammonium Maleate at 300° C.

A slurry of 9.8 g (0.1 mole) maleic anhydride was dissolved in 20 ml water at 80°-95° C. and stirred for 30 minutes while allowing the mixture to cool to 25° C. To this colorless solution at 25° C. was added 13 g of 30% aqueous solution of ammonium hydroxide (0.11 mol NH₃) to give a colorless solution. This solution was boiled to dryness over a period of 30 minutes at approximately 100°-115° C. to give a white crystalline solid. The solid was tumbled at 300° C. for 5 minutes to give a water insoluble, brick-red brittle grasslike solid weighing 9.6 g. This solid was dissolved in 40.0 g of an aqueous solution containing 3.8 g of sodium hydroxide to form a clear red-brown solution, pH 9.0, containing 25% solids.

FIG. 2 shows that the polyaspartic acid of this example in the calcium drift assay of Example 1 at 1.7 ppm was equivalent to that of thermally prepared polyaspartate.

In summary, polyaspartic acid prepared at 145°-150° C. from maleic anhydride and ammonia was ineffective as a scale inhibitor while that prepared at 190°-200° C. was nearly as effective as thermal polyaspartate and that prepared at 240° or 300° C. was equivalent to thermal polyaspartic as a scale inhibitor. The time required for polymerization was reduced from 4-8 hours to between 5 minutes and 1.5 hours, thus providing a significant improvement in the economy of industrial production.

EXAMPLE 6 Thermal Polymerization of Mono-Ammonium Fumarate at 145°-150° C.

Following the examples of U.S. Pat. No. 4,839,461, a slurry of 11.6 g (0.1 mole) fumaric acid was dissolved in 30 ml water was mixed with 13 g of 30% aqueous solution of ammonium hydroxide (0.11 mol NH₃). Carefully warming the slurry to boiling gave a dear solution. This solution was boiled to dryness over a period of 15 minutes to give a white crystalline solid. The solid was tumbled under nitrogen at 100 Torr, at 145°-150° C. for 8 hours to give an off-white glasslike solid weighing 13.2 g. This solid was dissolved in 40 g of an aqueous solution containing 4.0 g of sodium hydroxide to form a pale yellow solution, pH 8.5, containing 25% solids.

FIG. 3 shows a plot of the data obtained in the calcium drift assay on the material obtained in this example. The material was only slightly better than no additve when tested at 1.7 ppm.

EXAMPLE 7 Thermal Polymerization of Mono-Ammonium Fumarate at 190°-200° C.

A slurry of 11.6 g (0.1 mole) fumaric acid was dissolved in 30 ml water was mixed with 13 g of 30% aqueous solution of ammonium hydroxide (0.11 mol NH₃). Carefully warming the slurry to boiling gave a dear solution. This solution was boiled to dryness over a period of 15 minutes to give a white crystalline solid. The solid was tumbled under nitrogen at 100 Torr, at 190°-200° C. for 4 hours to give a water insoluble, tan grasslike solid weighing 12.0 g. This solid was dissolved in 40 g of an aqueous solution containing 4.0 g of sodium hydroxide to form a pale yellow solution, pH 7.0, containing 25% solids.

FIG. 3 shows a plot of the data obtained in the calcium drift assay on the material obtained in this example. The material was only slightly better than no additive when tested at 1.7 ppm.

EXAMPLE 8 Thermal Polymerization of Mono-Ammonium Fumarate at 240°-250° C.

A slurry of 11.6 g (0.1 mole) fumaric acid was dissolved in 30 ml water was mixed with 13 g of 30% aqueous solution of ammonium hydroxide (0.11 mol NH₃). Carefully warming the slurry to boiling gave a clear solution. This solution was boiled to dryness over a period of 15 minutes to give a white crystalline solid. The solid was tumbled under nitrogen at 100 Torr, at 240°-250° C. for 1.5 hours to give a water insoluble, dark brown glasslike solid weighing 9.3 g. This solid was dissolved in 40 g of an aqueous solution containing 4.0 g of sodium hydroxide to form a clear brown solution, pH 8.0, containing 25% solids.

FIG. 3 shows a plot of the data obtained in the calcium drift assay on the material obtained in this example. The material was much better than that prepared in Example 6 when tested at 1.7 ppm.

EXAMPLE 9 Thermal Polymerization of Mono-Ammonium Fumarate at 300° C.

A slurry of 11.6 g (0.1 mole) fumaric acid was dissolved in 30 ml water was mixed with 13 g of 30% aqueous solution of ammonium hydroxide (0.11 mol NH₃). Carefully warming the slurry to boiling gave a clear solution. This solution was boiled to dryness over a period of 15 minutes to give a white crystalline solid. The solid was tumbled at 300° C. for 5 minutes to give a water insoluble, dark brown grasslike solid weighing 9.8 g. This solid was dissolved in 40 g of an aqueous solution containing 3.8 g of sodium hydroxide to form a clear brown solution, pH 9.0, containing 25% solids.

FIG. 3 shows a plot of the data obtained in the calcium drift assay on the material obtained in this example. The material was much better than that prepared in Example 6 when tested at 1.7 ppm.

In summary, thermally polymerized mono-ammonium fumarate provided polyaspartate prepared at 145°-150° C. and at 190°-200° C. which was only slightly active in scale inhibition while that prepared at 240° C. and at 300° C. were active but less active than thermal polyaspartate as scale inhibitors.

EXAMPLE 10 Thermal Polymerization of Di-Ammonium Maleate at 135°-140° C.

Following the examples of U.S. Pat. No. 4,839,461, a solution of 1.96 g (0.02 mole) maleic anhydride was dissolved in 1 ml water at 25° C. and stiffed for 30 minutes while allowing the mixture to cool to 25° C. To this colorless solution at 25° C. was added 2.4 g of 30% aqueous solution of ammonium hydroxide (0.022 mol NH₃) to give a colorless solution. This solution was boiled to dryness over a period of 30 minutes at approximately 100°-120° C. and 10-20 Torr, to give a white crystalline solid. The solid was tumbled under nitrogen at 100 Torr, at 135°-140° C. for 8 hours to give a water insoluble, pinkish-tan brittle grasslike solid weighing 2.7 g. This solid was dissolved in 6.6 g of an aqueous solution containing 0.8 g of sodium hydroxide to form a clear orange solution, pH 7.0, containing 25% solids.

FIG. 4 shows a plot of the data obtained in this example compared to that of the no additive assay and the thermally prepared polyaspartate. The material obtained at 135°-145° C. is not as good as no additive when tested at 1.7 ppm.

EXAMPLE 11 Thermal Polymerization of Di-Ammonium Maleate at 240°-250° C.

A solution of 9.8 g (0.1 mole) maleic anhydride was dissolved in 20 ml water at 50°-60° C. and stirred for 30 minutes while allowing the mixture to cool to 25° C. To this colorless solution at 25° C. was added 26 g of 30% aqueous solution of ammonium hydroxide (0.22 mol NH₃) to give a colorless solution. This solution was boiled to dryness over a period of 30 minutes at approximately 100°-120° C. and 10-20 Torr, to give a white crystalline solid. The solid was tumbled under nitrogen at 100 Torr, at 240°-250° C. for 1.5 hours to give a water insoluble, red-brown brittle grasslike solid weighing 9.4 g. This solid was dissolved in 40 g of an aqueous solution containing 3.8 g of sodium hydroxide to form a dear red-brown solution, pH 7.0, containing 25% solids.

FIG. 4 shows a plot of the data obtained in this example compared to that of the no additive assay and the thermally prepared polyaspartate. The material of this example is equivalent to that of thermal polyaspartate when tested at 1.7 ppm.

EXAMPLE 12 Thermal Polymerization of Di-Ammonium Fumarate at 140°-150° C.

A slurry of 11.6 g (0.1 mole) fumaric acid was dissolved in 30 ml water was mixed with 26 g of 30% aqueous solution of ammonium hydroxide (0.22 mol NH₃). Carefully warming the slurry to boiling gave a clear solution. This solution was boiled to dryness over a period of 15 minutes to give a white crystalline solid. The solid was tumbled under nitrogen at 100 Torr, at 140°-150° C. for 8 hours to give a water insoluble, brown, grasslike solid weighing 14 g. This solid was dissolved in 100 g of an aqueous solution containing 2.0 g of sodium hydroxide to form a pale yellow solution, pH 7.0, containing 25% solids.

FIG. 4 shows a plot of the data obtained in the calcium drift assay on the material obtained in this example. The material was only slightly better than no additve when tested at 1.7 ppm.

EXAMPLE 13 Thermal Polymerization of Di-Ammonium Fumarate at 235°-245° C.

A slurry of 11.6 g (0.1 mole) fumaric acid was dissolved in 30 ml water was mixed with 26 g of 30% aqueous solution of ammonium hydroxide (0.22 mol NH₃). Carefully warming the slurry to boiling gave a dear solution. This solution was boded to dryness over a period of 15 minutes to give a white crystalline solid. The solid was tumbled under nitrogen at 100 Torr, at 235°-245° C. for 1.5 hours to give a water insoluble, brown, grasslike solid weighing 9.0 g. This solid was dissolved in 100 g of an aqueous solution containing 2.0 g of sodium hydroxide to form a pale yellow solution, pH 8.5, containing 25% solids.

FIG. 4 shows a plot of the data obtained in the calcium drift assay on the material obtained in this example. The material was only slightly better than no additve when tested at 1.7 ppm.

EXAMPLE 14 Molecular Weight Analysis of Polyaspartate Prepared in Various Ways

Molecular weight determination of the materials prepared in the foregoing examples and commercially available materials was made by chromatography on a 1 cm×18 cm, Sephadex G-50 column in a mobile phase of 0.02 M sodium phosphate buffer, pH 7.0, running at 0.5 ml/min, with detection in the UV at 240 nm. The sample size ranged from 0.01 to 0.5 mg/ml.

FIG. 5 shows the results of sodium polyaspartate, 13,000 m.w., from Sigma, I; sodium polyaspartate, 7,500 m.w., from Sigma, II; and sodium polyaspartate, Example 1, II. m.w. 5,000, from Sigma.

FIG. 6 shows the result of Example 4 as "a"; Example 11 as "b"; Example 2 as "c" and Example 10 as "d". With maleic acid and ammonia reactions, temperatures of 240° C. gave molecular weights over a broad range centered at 7,000-8,000 while temperatures of 135°-150° C. gave molecular weights over a broad range centered at 2,000.

FIG. 7 shows the result of Example 8 as "e"; Example 13 as "f"; Example 6 as "g" and Example 12 as "h". With fumaric acid and ammonia reactions, temperatures of 240° C. gave molecular weights over a broad range centered at 7,000-8,000 while temperatures of 140°-150° C. gave molecular weights over a broad range centered at 2,000.

FIG. 8 shows the result of Example 3 as "i"; Example 7 as "j". Temperatures of 190°-200° C. gave molecular weights for maleate over a broad range centered at 7,000-8,000 while temperatures of 190°-200° C. for fumarate gave molecular weights over a broad range centered at 2,000. 

I claim:
 1. A process for the preparation of polysuccinimide comprising reacting maleic acid and ammonia in a molar ratio of 1:1-2.1, heating to remove water forming a melt of maleic acid and ammonia, removing water as the reaction proceeds and bringing the temperature to 190° to 300° C. to form said polysuccinimide.
 2. The process of claim 1, wherein the temperature is brought to 200 to 300° C.
 3. The process of claim 1, wherein the temperature is brought to 240 to 300° C.
 4. The process of claim 1, wherein the temperature is brought to 190 to 300° C. for a time of four hours or less.
 5. A process for the preparation of polysuccinimide comprising reacting fumaric acid and ammonia in a molar ratio of 1:1-2.1, heating the obtained solution to remove water, removing water as the reaction proceeds and bringing the temperature to 190 to 300° C. to form said polysuccinimide.
 6. The process of claim 5, wherein the temperature is brought to 200 to 300° C.
 7. The process of claim 5, wherein the temperature is brought to 240 to 300° C.
 8. The process of claim 5, wherein the temperature is brought to 190 to 300° C. for a time of four hours or less. 